JPS5813634A - Preparation of thermosetting resin molding material - Google Patents
Preparation of thermosetting resin molding materialInfo
- Publication number
- JPS5813634A JPS5813634A JP11121281A JP11121281A JPS5813634A JP S5813634 A JPS5813634 A JP S5813634A JP 11121281 A JP11121281 A JP 11121281A JP 11121281 A JP11121281 A JP 11121281A JP S5813634 A JPS5813634 A JP S5813634A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- molding material
- dehydrator
- resin molding
- reduced pressure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は熱硬化性樹脂成形材料の製造方法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a thermosetting resin molding material.
一般に熱硬化性樹脂成形材料は、樹脂シラツブを各種の
バッチ式や連続式の真空乾燥域に送り込んで、ここで縮
重合物を乾燥させて得られるものであるが、従来の乾燥
方式は樹脂シうツブをタンクに溜め九まま中或いは薄膜
状に引き延ばし良状態で乾燥させるものであるため、脱
水後の縮重合物は5.?301111の大径の粒状とな
り、樹脂成形材料とするためKは、更に粉砕工程を加え
なければならないという問題があ秒、特にユリア樹脂の
場合社、融点が90’011J後である丸め、通常の粉
砕機では粉砕に併う熱によって粉砕が困難になるという
問題があった。Generally, thermosetting resin molding materials are obtained by feeding resin sills into various batch-type or continuous-type vacuum drying areas, where the condensation product is dried, but the conventional drying method is The condensation product after dehydration is rated at 5.5% because the sludge is stored in a tank and then stretched out in a vacuum or in a thin film and dried in good condition. ? 301111 becomes large-diameter granules, and in order to use it as a resin molding material, K has the problem of having to undergo an additional pulverization process.Especially in the case of urea resin, the melting point is after 90'011J. The problem with a crusher is that the heat involved in crushing makes crushing difficult.
本郵明紘上記の点く鑑みて為されたものであって、主な
目的とするところは、0.25sm以下程度の粒度の小
さな樹ms末を得ることができる熱硬化樹脂成形材料の
製造方法を提供することである。This postal service was created in view of the above points, and its main purpose is to produce a thermosetting resin molding material that can obtain small particle size particles of about 0.25 sm or less. The purpose is to provide a method.
本発明を以下図に示す実施例に基づいて詳述する。本発
明に係る熱硬化性樹脂成形材料の製造方法呟、樹脂シう
ツブを減圧下で噴霧させると共に加熱して縮重合物を脱
水させて樹脂粉末を得る仁とを特徴とするものである。The present invention will be described in detail below based on embodiments shown in the figures. The method for producing a thermosetting resin molding material according to the present invention is characterized by spraying a resin film under reduced pressure and heating it to dehydrate the condensation product to obtain a resin powder.
樹脂シラツブ(1)は、例えばユリア樹脂では、本ルマ
リンと尿素と適当な触媒を反応させて得られる初期縮合
物である糊状の液体にバルブなどの充填材が混入された
ものであり、ユリア樹脂の場合自由氷分が401111
mに調製されたものが用いられ、図に示すように、シラ
ッづタンク(2)に貯えられ、供給ポンプ(s)によっ
て噴霧式脱水機(4)K送られる。*WiIシラツブ(
1)は脱水機14)に送られる前に予備加熱機:湯)に
よって予熱され、真空ポンプ(6)により内部が減圧さ
れた脱水411nlの上端のノズル(7)より噴霧され
、樹脂シラツブ(1)の霧が脱水機(4)の周囲に設は
九ヒータ(8)の加熱によって乾燥され、その結果自由
水分が3畳以下に脱水され丸線重合物が得られ、脱水機
(4)下部に貯るこの縮重合物を脱水機(4)下端に設
けたロータリーバルブやタプルバンパーなどの取出口(
9)より樹脂粉末(l菊として取出すものである。ここ
で上記のヒータ(8)としては、減圧下、特に真空中で
は輻射熱あるいは水分子に直接作用さ、せるものしかヒ
ータとしての効果がない丸め、赤外線ランプや高周波加
熱装置が用いられる。このようにして得られるユリアI
Il!脂の*脂粉末Fi60mesh以下、すなわち粒
径が0.25a以下のものであり、別途に粉砕を行うこ
となくそのまま樹脂成形材料として使用される。尚、脱
水機(4)・内で蒸発する水分や溶剤はフン4ンサやコ
ールドトラップのような捕集器(至)へ上記の真空ボン
づ+8)の作用によって′吸引され、ここで凝集された
後、凝集液タンク(1N)内に送られてここに貯えられ
る。図中(I憤は真空ポンプ1ttlと凝集液タンク(
11)との間に配設した真空ポンプ用タンクである。Resin silub (1), for example, in the case of urea resin, is a paste-like liquid that is an initial condensate obtained by reacting real lumaline, urea, and a suitable catalyst, with fillers such as valves mixed therein. In the case of resin, the free ice content is 401111
As shown in the figure, the prepared water is stored in a Shiratzu tank (2) and sent to a spray dehydrator (4)K by a supply pump (s). *WiI Shiratsubu (
1) is preheated by a preheater (hot water) before being sent to the dehydrator 14), and is sprayed from the nozzle (7) at the upper end of the dehydrated 411nl whose interior is depressurized by the vacuum pump (6). ) is dried by the heating of the nine heaters (8) installed around the dehydrator (4), and as a result, the free water is dehydrated to less than 3 tatami and a round polymer is obtained, and the lower part of the dehydrator (4) This condensation product accumulated in
The resin powder (1 chrysanthemum) is extracted from the resin powder (9).The heater (8) mentioned above is only effective as a heater by directly acting on radiant heat or water molecules under reduced pressure, especially in a vacuum. Rounding, an infrared lamp or a high frequency heating device is used.Uria I obtained in this way
Il! The fat powder Fi60mesh or less, that is, the particle size is 0.25a or less, and can be used as a resin molding material as it is without being separately pulverized. The water and solvent that evaporate inside the dehydrator (4) are sucked into a collector (to) such as a funnel or cold trap by the action of the vacuum bong +8) mentioned above, where they are coagulated. After that, it is sent to the flocculation liquid tank (1N) and stored there. In the diagram (I) the vacuum pump 1ttl and the flocculating liquid tank (
11) is a vacuum pump tank installed between the
本発明は以上のように、樹脂シ5ツづを減圧下で噴霧さ
せると共に加熱して縮重合物を脱水させるものであるか
ら、縮重合物が霧の状瑠の微細な粒子の1壕で乾燥され
ることとな抄、その結果、縮重合物を脱水させて得られ
るSt脂粉末の粒径を小さくすることができ、別途の粉
砕工穆を経ることなく、そのtま樹脂成形材料として使
用できるという利点がある。As described above, the present invention dehydrates the condensation polymer by spraying five pieces of resin under reduced pressure and heating it, so that the condensation polymer is formed in one hole of fine particles in the form of mist. As a result, the particle size of the St fat powder obtained by dehydrating the condensation polymer can be reduced, and it can be used as a resin molding material without going through a separate crushing process. It has the advantage of being usable.
図面は本発明の一実施例を示す概略工程図であり、(1
)は樹脂シラツブ、14)は噴霧式脱水機、◆鴫は樹脂
粉末である6
代理人 弁−士 石 1)長 七The drawings are schematic process diagrams showing one embodiment of the present invention, and (1
) is a resin shiratsubu, 14) is a spray dehydrator, and ◆ is a resin powder. 6 Agent Ben-shi Ishi 1) Choshichi
Claims (1)
熱して縮重合物を脱水させて樹脂粉末を得ることを特徴
とする熱硬化性fIIIFl&成形材料の製造方法(1) A method for producing thermosetting fIIIFl & molding material, which comprises spraying resin silub under reduced pressure and heating to dehydrate the condensation product to obtain resin powder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11121281A JPS5813634A (en) | 1981-07-15 | 1981-07-15 | Preparation of thermosetting resin molding material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11121281A JPS5813634A (en) | 1981-07-15 | 1981-07-15 | Preparation of thermosetting resin molding material |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5813634A true JPS5813634A (en) | 1983-01-26 |
Family
ID=14555360
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11121281A Pending JPS5813634A (en) | 1981-07-15 | 1981-07-15 | Preparation of thermosetting resin molding material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5813634A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5624530A (en) * | 1993-05-11 | 1997-04-29 | Ultrasonic Dryer, Ltd. | Spray drying system |
-
1981
- 1981-07-15 JP JP11121281A patent/JPS5813634A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5624530A (en) * | 1993-05-11 | 1997-04-29 | Ultrasonic Dryer, Ltd. | Spray drying system |
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